GB2206990A - Separator for electrochemical cells - Google Patents

Separator for electrochemical cells Download PDF

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Publication number
GB2206990A
GB2206990A GB08808823A GB8808823A GB2206990A GB 2206990 A GB2206990 A GB 2206990A GB 08808823 A GB08808823 A GB 08808823A GB 8808823 A GB8808823 A GB 8808823A GB 2206990 A GB2206990 A GB 2206990A
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GB
United Kingdom
Prior art keywords
separator
anode
cathode
electrochemical cell
cells
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Granted
Application number
GB08808823A
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GB8808823D0 (en
GB2206990B (en
Inventor
Rowland Allan Griffin
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Duracell Inc USA
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Duracell International Inc
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Publication date
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Publication of GB8808823D0 publication Critical patent/GB8808823D0/en
Publication of GB2206990A publication Critical patent/GB2206990A/en
Application granted granted Critical
Publication of GB2206990B publication Critical patent/GB2206990B/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M6/00Primary cells; Manufacture thereof
    • H01M6/02Details
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M6/00Primary cells; Manufacture thereof
    • H01M6/14Cells with non-aqueous electrolyte
    • H01M6/16Cells with non-aqueous electrolyte with organic electrolyte
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/38Selection of substances as active materials, active masses, active liquids of elements or alloys
    • H01M4/381Alkaline or alkaline earth metals elements
    • H01M4/382Lithium
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/50Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409Separators, membranes or diaphragms characterised by the material
    • H01M50/411Organic material
    • H01M50/414Synthetic resins, e.g. thermoplastics or thermosetting resins
    • H01M50/417Polyolefins
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/463Separators, membranes or diaphragms characterised by their shape
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/489Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
    • H01M50/491Porosity
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M6/00Primary cells; Manufacture thereof
    • H01M6/14Cells with non-aqueous electrolyte
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0017Non-aqueous electrolytes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0017Non-aqueous electrolytes
    • H01M2300/0025Organic electrolyte
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Inorganic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Cell Separators (AREA)
  • Primary Cells (AREA)
  • Secondary Cells (AREA)
  • Battery Electrode And Active Subsutance (AREA)
  • Apparatuses For Bulk Treatment Of Fruits And Vegetables And Apparatuses For Preparing Feeds (AREA)
  • Preparation Of Fruits And Vegetables (AREA)

Description

SEPARATOR FOR ELECTROCHEMICAL CELLS Zir; 0 4G6920 This invention relates
to a separator for non-aqueous electrochemical cells and in particular lithium/manganese dioxide cells. It has been discovered that a polypropylene microporous film having a thickness greater than one mil and voids greater than 50% by volume, has beneficial properties without the concomitant problems generally associated with separators "having open structures.
Separators are critical to an electrochemical cell because they provide a physical barrier which prevents short circuits between the electrodes. At the sime time a separator must have some porosity in order that electrolyte can occupy the pores to provide a reservoir of electrolyte between the electrodes. The thickness of the separator determines the distance between the electrodes, which in turn determines the resistivity of the electrolyte therebetween. Therefore, in order to minimize the electrolyte resistance it is normally considered desirable to use a thin separator. A thinner separator also permits more active material to be used in the cell.
Non-aqueous electrolytes are generally much less conductive than aqueous electrolytes. Therefore non-aqueous cells must use thinner separators than can be tolerated in aqueous cells in order to minimize the electrolyte resistance. Further, a separator useful in an alkaline cell may not be compatible with the chemicals in a non-aqueous cell. As a result, a separator which has utility in an aqueous cell is generally not useful in a non-aqueous cell.
The porosity of a separator is important in that it must be high enough to provide sufficient electrolyte between the electrodes. However, if the porosity is too high the mechanical integrity of the separator decreases and it becomes subject to tearing or breaking during manufacture. One example of a widely used commercially available separator is Celgard 2400 (Questar Corp.). This is a one mil microporous polypropylene film having 38% porosity. Another commercially available separator is Celgard 2500 which is a one mil microporous polypropylene film having 45% porosity. It is believed that the Celgard 2500 has the highest porosity of all commercially available microporous polypropylene separators.
Porosity of separators has been found to have an impact on cell safety. When a cell is abused (i.e. short circuited) it generates internal beat. As the internal temperature approaches the melting point of the polyolefin the micropores begin to close a.s the separator begins to melt. This results in a partial shut down of the short circuit current of the cell, which slows down the generation of heat so that the cell is less likely to vent. It is generally believed that if separators having a more porous structure than those now in common use were used. the shut down characteristics would be adversely effected. This is because it has been believed that the pores would not be closed and also because some films would tend to shrink as they melt or soften. This would enable the electrodes to physically contact each other thereby increasing the short circuit problems of the cell. Rather than shutting down the flow of current and ameliorating the resulting heating, it was believed that cells using such separators would continue to heat and cause the cell to vent. Microporous films made from polymers which exhibit significantly different densities between their crystalline and amorphous phases, such as polyethylene, are generally believed to be prone to the shrink a ge problem regardless of the porosity. Films made from polymers which do not have a significant difference 1 - i 1 1 i 1 1 between the densities of the crystalline and amorphous phases, such as polypropylene, appear to exhibit less of a shrinkage problem.
US patent 4,335,193 discloses filled microporous films having porosities as high as 75% for use in aqueous electrochemical systems such as the lead acid type. In practice, with respect to non-aqueous systems, it has been found that filled microporous films do not shut down when a cell is short circuited. It is believed that this is due to the structural support imparted to the separator by the filler. Accordingly, these films are considered highly undesirable for use in non-aqueous cells. Therefore, a separator such as Celgard 2400 has been widely used in non-aqueous cells because its porosity is about as high as is commercially available for unfilled microporous films. Its 38% porosity has been adopted as a standard for the lithium/manganese dioxide and other cell types and has been considered heretofore to be the preferred separator in terms of cell performance, while ensuring partial shut down without shrinkage during short circuit abuse..
Unfilled separators having higher porosities than those of the film types discussed above are available with non-woven fibrous separators. Nonwoven fibrous separators can have porosities in the range of 60-80%. However, these materials are generally not useful for many cell environments, especially when the electrodes with separator therebetween are tightly wound together e.g. lithium/manganese dioxide, because their open structure permits short circuits between the electrodes. To minimize the short circuit problem these separators have to be used In thicknesses of at least 6 mils. The increased separator thickness increases the resistance of electrolyte between the electrodes and takes up space which could otherwise be filled with active material whereupon the energy density would be impaired.
Microporous films of the type discussed above are used most frequently in the non-aqueous electrochemical systems. Typical of these is lithium/ manganese dioxide. Within the past few years the production of lithium/manganese dioxide has increased dramatically. As production levels have increased, it has been found that in a small percentage of cells soft shorts' occur.
A soft short is a high resistance short as distinguished from a direct short circuit. It occurs when there is a high resistance contact between the electrodes. Apparently, a particle of manganese dioxide can partially penetrate through the thin one mil Celgard 2400 separator permitting electrical contact with the anode. Since manganese dioxide is a semiconductor, this is not a zero resistance short circuit. The effect of a soft short is to slowly drain the cell until it is totally discharged. The use of thicker separators would reduce the occurrence of soft shorts but thicker separators would also cause anundesirable increase in the internal resistance of the cell.
At Applicant's: request an experimental microporous polypropylene film which is 1.5 mil thick and has 33% voids was made by a commercial supplier. Applicant tried this separator in experimental cells and found that the room temperature performance was comparable to cells with a one mil separator having 38% voids. However, it was not until Applicant tested cells at low temperature e.g. -20 0 C that it was discovered that performance was adversely affected. This was attributed to the increased electrolyte resistance because of the greater thickness. This suggests that the trade off for improved cell reliability by using a thicker separator will be a decrease in low temperature performance.
It has now been discovered that lithiumimanganese dioxide cells using as separator material a microporous polypropylene film having a thickness between i i i i i i i i i i i i 1 1 1. 1 and 4 mi l, and preferably 1. 5 to 3 mi Is, but with at least 45%, and preferably 50-80%, and more preferably 55-70% voids performs in all respects. including low temperature discharge, at least as well as the commercially available one mil polypropylene separator with 38% voids.
The features and advantages of the present Invention are evident upon consideration of the following examples.
Examele 1 The test cell for this a.nd the following examples is a 2/3A size Li/MnO 2 cell. The cell uses a lithium foil anode, and an MnO2 cathode having 10% by weight carbon as a conductive agent and 5% PTFE as binder. The electrodes are spirally wound with the separator interposed therebetween. The spirally wound electrodes and sep4.rator are inserted into an open ended can. The cell is filled with a non-aqueous electrolyte comprised of 1 M LiCF3503 in an approximately 1:1 ratio of propylene carbonateldioxolane. An electrically isolated cover is sealed on the open end of the cell. The electrodes are connected to the cell can and cover respectively.
Five identical cells are built as described above, except that the separator in three cells is a polypropylene microporous film that is 1.5 mil thick and has a porosity of 33% while the other two use a microporous polypropylene film that is one mil thick and has a porosity of 38%(Celgard 2400). All five cells are tested using a low temperature (- 200C_) pulse regime of 1.2 amps for 3 seconds followed by 7 seconds off. All three cells having the thicker separator deliver an average of 33% fewer pulses to a one volt cutoff 1 1 than cells having the Celgard 2400 separator. AS both separators have roughly the same porosity this ex amp] e demonstrates the adverse impact on low temperature performance of separators thicker than one mil.
I Example 2
Two cells are built using a separator comprised of Celgard 2400 and three cells are built using a separator comprising a polypropylene m-lcroporous film that is 1.8 mil thick and has a porosity of 62%. The three cells using the thicker separator give an average of 39% more pulses to a one volt cutoff than the three cells using the thinner separator. This example demonstrates unexpected beneficial. performance characteristics of cells using thicker separators with a higher porosity.
Example 3
Two cells are bvilt using Celgard 2400 and three cells are built using a polypropylene microporous film 1.3 mil thick and 60% porosity. The cells using the thicker separator perform as well as the cells using Celgard 2400 under the low temperature pulse test.
i Example 4
Two cells are built using a polypropylene microporous, separator that is 2.5 mil thick and 55% porous. These cells deliver over 300 pulses to a one volt cut-off under the low temperature pulse test. A The previous ex&nples clearly demonstrate the performance benefits of cells using microporous polypropylene separators having a thickness between 1.1 and 3 1 mils and a Porosity of between 50% and 80. While a MicrOporous separator with these voids but with a thickness of 4 mil or greater would be operable, such thicknesses are not preferred because the separator would take up too much space.
Because of the greater thickness over Celgard 2400, the separators of the present invention are expected to reduce the scrap rate of cells due to soft shorts without detrimentally affecting the low temperature performance. The separators encompassed by the present invention offer a significant advancement in the manufacture of spirally wound lithium/manganese dioxide cells.
1 1 i 8

Claims (6)

CLAIMS:
1. An electrochemical cell comprising an anode comprised of lithium; a cathode compri sed of manganese dioxide; and a non-aqueous electrolyte; wherein said separator is comprised of a microporous polypropylene film having a thickness between 1.1 and 4.0 mils and internal voids of between 50% and 80% by volume.
2. The electrochemical cell of claim 1 wherein the thickness of the separator is between 1.5 and 3 mils.
3. The electrochemical cell of claim 1 or 2 wherein the internal voids are between 55% and 70% by volume.
4. The electrochemical cell of claim 1. 2 or 3 wherein the anode, the cathode. and the separator are spirally wound together with the separator between the anode and cathode.
5. An electrochemical cell comprising a sealed casing; an anode. a cathode. a separator positioned between said anode and said cathode, and a non-aqueous electrolyte sealed in said casing; and a pair of electrical terminals electrically isolated from each other and i i I i i i Al, 9 electrically connected to the anode and the cathode respectively; wherein the anode is comprised of lithium foil, the cathode is comprised of manganese dioxide. and said separator consists essentially of a microporous polypropylene film having a thickness of about 1.5 mils and internal voids of about 60% by volume; wherein said anode, cathode, and separator are spirally wound together in a "swiss roll" configuration.
6. An electrochemical cell as claimed in claim 2 and substantially as set forth in any of the foregoing examples.
Published 19b13 at The Patent Offire. State House. 6671 High Holborn, London WC1R 4TP. Farther copies may be obtained from The Patent Mce, SOeS Brareb- St Ma:-Y Cray. Orpington, Kent. BR5 3RD. T-rinted by Multp.ex cechnicries ltd, St Mary Cray. Kent. Con 1'87-
GB8808823A 1987-07-17 1988-04-14 Separator for electrochemical cells Expired - Lifetime GB2206990B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US07/074,590 US4794057A (en) 1987-07-17 1987-07-17 Separator for electrochemical cells

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GB8808823D0 GB8808823D0 (en) 1988-05-18
GB2206990A true GB2206990A (en) 1989-01-18
GB2206990B GB2206990B (en) 1990-11-28

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US (1) US4794057A (en)
JP (1) JPS6435872A (en)
KR (1) KR890003055A (en)
AR (1) AR240212A1 (en)
AU (1) AU1470788A (en)
BE (1) BE1001677A3 (en)
BR (1) BR8802351A (en)
CA (1) CA1315843C (en)
CH (1) CH675794A5 (en)
DE (1) DE3824101C2 (en)
DK (1) DK395988A (en)
ES (1) ES2007232A6 (en)
FR (2) FR2618259B1 (en)
GB (1) GB2206990B (en)
HK (1) HK19294A (en)
IL (1) IL86034A0 (en)
IT (1) IT1219386B (en)
NL (1) NL8801216A (en)
NO (1) NO883153L (en)
SE (1) SE8802633L (en)
ZA (1) ZA882785B (en)

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GB2314200A (en) * 1996-06-11 1997-12-17 Samsung Display Devices Co Ltd A group of winding electrodes
US5888667A (en) * 1996-06-19 1999-03-30 Samsung Display Devices Co., Ltd. Separator for jelly-roll type electrode

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US5176968A (en) * 1990-12-27 1993-01-05 Duracell Inc. Electrochemical cell
US5290414A (en) * 1992-05-15 1994-03-01 Eveready Battery Company, Inc. Separator/electrolyte combination for a nonaqueous cell
US5368958A (en) * 1992-08-20 1994-11-29 Advanced Energy Technologies Incorporated Lithium anode with conductive for and anode tab for rechargeable lithium battery
US5700599A (en) * 1996-01-12 1997-12-23 Danko; Thomas High absorption rate battery separator
US5700600A (en) * 1996-01-12 1997-12-23 Danko; Thomas Long life battery separator
US5962162A (en) * 1997-10-10 1999-10-05 Ultralife Batteries Inc. Lithium ion polymer cell separator
US5958088A (en) * 1998-03-04 1999-09-28 Duracell, Inc. Prismatic cell construction
US6670074B2 (en) * 2001-04-23 2003-12-30 Wilson Greatbatch Ltd. Glass to metal seal
US6849360B2 (en) 2002-06-05 2005-02-01 Eveready Battery Company, Inc. Nonaqueous electrochemical cell with improved energy density
US8465860B2 (en) * 2008-01-23 2013-06-18 The Gillette Company Lithium cell
US8273483B2 (en) * 2008-02-14 2012-09-25 The Gillette Company Lithium cell
US20090214950A1 (en) * 2008-02-22 2009-08-27 Bowden William L Lithium cell
US8076028B2 (en) * 2008-04-16 2011-12-13 The Gillette Company Lithium cell with cathode including iron disulfide and iron sulfide
US8859145B2 (en) * 2008-05-23 2014-10-14 The Gillette Company Method of preparing cathode containing iron disulfide for a lithium cell
US20090317725A1 (en) * 2008-06-23 2009-12-24 Zhiping Jiang Lithium cell with cathode containing iron disulfide
US8153296B2 (en) * 2008-08-27 2012-04-10 The Gillette Company Lithium cell with cathode containing metal doped iron sulfide
US8076029B2 (en) * 2009-01-20 2011-12-13 The Gillette Company Lithium cell with iron disulfide cathode and improved electrolyte
US20100203370A1 (en) * 2009-02-12 2010-08-12 Michael Pozin Lithium cell with iron disulfide cathode
US8048562B2 (en) * 2009-03-27 2011-11-01 The Gillette Company Lithium cell with improved iron disulfide cathode
WO2011063132A1 (en) * 2009-11-18 2011-05-26 A123 Systems, Inc. Composite separator for electrochemical cell and method for its manufacture
US9383593B2 (en) * 2014-08-21 2016-07-05 Johnson & Johnson Vision Care, Inc. Methods to form biocompatible energization elements for biomedical devices comprising laminates and placed separators
JP6974641B1 (en) * 2021-03-31 2021-12-01 日本たばこ産業株式会社 Induction heating device, its control unit, and its operation method
JP6967169B1 (en) 2021-03-31 2021-11-17 日本たばこ産業株式会社 Induction heating device and its operation method

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2314200A (en) * 1996-06-11 1997-12-17 Samsung Display Devices Co Ltd A group of winding electrodes
GB2314200B (en) * 1996-06-11 1999-06-16 Samsung Display Devices Co Ltd A group of winding electrodes
US5932370A (en) * 1996-06-11 1999-08-03 Samsung Display Devices Co., Ltd. Group of winding electrodes
US5888667A (en) * 1996-06-19 1999-03-30 Samsung Display Devices Co., Ltd. Separator for jelly-roll type electrode

Also Published As

Publication number Publication date
CH675794A5 (en) 1990-10-31
FR2618057A1 (en) 1989-01-20
AR240212A1 (en) 1990-02-28
DK395988A (en) 1989-01-18
NL8801216A (en) 1989-02-16
DE3824101C2 (en) 1998-01-15
AU1470788A (en) 1989-01-19
NO883153L (en) 1989-01-18
HK19294A (en) 1994-03-18
GB8808823D0 (en) 1988-05-18
CA1315843C (en) 1993-04-06
FR2618259B1 (en) 1990-08-24
DE3824101A1 (en) 1989-01-26
JPS6435872A (en) 1989-02-06
ZA882785B (en) 1989-12-27
SE8802633L (en) 1989-01-18
GB2206990B (en) 1990-11-28
FR2618057B1 (en) 1992-03-06
BE1001677A3 (en) 1990-02-06
US4794057A (en) 1988-12-27
SE8802633D0 (en) 1988-07-14
IT8867574A0 (en) 1988-06-17
IL86034A0 (en) 1988-09-30
ES2007232A6 (en) 1989-06-01
NO883153D0 (en) 1988-07-15
IT1219386B (en) 1990-05-11
FR2618259A1 (en) 1989-01-20
KR890003055A (en) 1989-04-12
BR8802351A (en) 1989-02-08
DK395988D0 (en) 1988-07-15

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Expiry date: 20080413